Method of forming membranes useful for separation of gases

Claim 1

A method of separating a charge gas mixture containing a more permeable gas and less permeable gas which comprises passing a charge gas mixture containing a more permeable gas and a less permeable gas into contact with a membrane of a high purity alumina containing aluminum-oxygen repeating units and characterized by a thickness of 8-200 microns and a narrow pore size distribution wherein at least about 70% of the pores have a Pore Radius of less than about 1000 Å; maintaining a pressure on the charge side of said membrane greater than the pressure on the permeate side of said membrane thereby yielding a permeate containing increased quantity of said more permeable gas and decreased quantity of said less permeable gas and a retentate containing decreased quantity of said more permeable gas and an increased quantity of said less permeable gas; recovering said permeate containing increased quantity of said more permeable gas and decreased quantity of said less permeable gas; and recovering said retentate containing decreased quantity of said more permeable and an increased quantity of said less permeable gas.

Claim 2

A method of separating a charge gas mixture containing a more permeable gas and less permeable gas which comprises passing a charge gas mixture containing a more permeable gas and a less permeable gas into contact with a membrane of a high purity alumina containing aluminum-oxygen repeating units and characterized by a thickness of 8-200 microns and a narrow pore size distribution wherein at least about 70% of the pores have a Pore Radius of less than about 1000 Å; maintaining a pressure on the charge side of said membrane greater than the pressure on the permeate side of said membrane thereby yielding a permeate containing increased quantity of said more permeable gas and decreased quantity of said less permeable gas and a retentate containing decreased quantity of said more permeable gas and an increased quantity of said less permeable gas; recovering said permeate containing increased quantity of said more permeable gas and decreased quantity of said less permeable gas; and recovering said retentate containing decreased quantity of said more permeable and an increased quantity of said less permeable gas.

Claim 7

The method of preparing a membrane assembly containing (i) a porous ceramic carrier layer characterized by mechanical strength and (ii) a porous surface layer which comprises loading the outer layers of macropores of a porous ceramic carrier with blocking liquid thereby forming a porous ceramic support layer bearing outer layers of macropores loaded with adsorbed blocking liquid; contacting said outer layers of macropores of said porous ceramic carrier layer, with adsorbed blocking liquid with an aluminum alkoxide sol containing peptizing agent; maintaining said outer layers of macropores of said porous carrier layer loaded with adsorbed blocking liquid in contact with said aluminum alkoxide sol for an adsorption period during which said alkoxide sol is adsorbed as a surface layer on the surface of said porous carrier layer; drying said porous support layer bearing (i) outer layers of macropores loaded with adsorbed blocking liquid and (ii) a surface layer of said alkoxide sol during a controlled drying period during which said adsorbed blocking liquid migrates outwardly toward the surface of said porous ceramic carrier layer during drying and minimizes migration of said alkoxide sol into said porous ceramic carrier layer as drying continues thereby forming a dried porous ceramic carrier layer bearing a surface layer of dried alkoxide sol; calcining said porous ceramic carrier layer bearing said surface layer of dried alkoxide sol at a calcining temperature of 400° C.-500° C. thereby decomposing said alkoxide and forming a porous carrier layer bearing a surface layer of decomposed alkoxide sol; and recovering said porous ceramic carrier layer bearing a surface layer of decomposed alkoxide sol.

Claim 8

The method of preparing a membrane assembly containing (i) a porous ceramic carrier layer characterized by mechanical strength and (ii) a porous surface layer which comprises loading the outer layers of macropores of a porous ceramic carrier with blocking liquid thereby forming a porous ceramic support layer bearing outer layers of macropores loaded with adsorbed blocking liquid; contacting said outer layers of macropores of said porous ceramic carrier layer, with adsorbed blocking liquid with an aluminum alkoxide sol containing peptizing agent; maintaining said outer layers of macropores of said porous carrier layer loaded with adsorbed blocking liquid in contact with said aluminum alkoxide sol for an adsorption period during which said alkoxide sol is adsorbed as a surface layer on the surface of said porous carrier layer; drying said porous support layer bearing (i) outer layers of macropores loaded with adsorbed blocking liquid and (ii) a surface layer of said alkoxide sol during a controlled drying period during which said adsorbed blocking liquid migrates outwardly toward the surface of said porous ceramic carrier layer during drying and minimizes migration of said alkoxide sol into said porous ceramic carrier layer as drying continues thereby forming a dried porous ceramic carrier layer bearing a surface layer of dried alkoxide sol; calcining said porous ceramic carrier layer bearing said surface layer of dried alkoxide sol at a calcining temperature of 400° C.-500° C. thereby decomposing said alkoxide and forming a porous carrier layer bearing a surface layer of decomposed alkoxide sol; and recovering said porous ceramic carrier layer bearing a surface layer of decomposed alkoxide sol.

Claim 16

The method of preparing a membrane assembly containing (i) a porous ceramic carrier layer characterized by mechanical strength and (ii) a porous surface layer which comprises loading the outer layers of macropore of a porous ceramic carrier with ethanol blocking liquid thereby forming a porous ceramic support layer bearing outer layers of macropores loaded with adsorbed blocking liquid; contacting said outer layers of macropores of said porous ceramic carrier layer loaded with said ethanol adsorbed blocking liquid with an aluminum tri-isopropoxide sol; maintaining said outer layers of macropores of said porous carrier layer loaded with said ethanol adsorbed blocking liquid in contact with said aluminum tri-isopropoxide sol for an adsorption period during which said sol is adsorbed as a surface layer on the surface of said porous carrier layer; drying said porous support layer bearing (i) outer layers of macropores loaded with said ethanol adsorbed blocking liquid and (ii) a surface layer of said aluminum tri-isoproxide sol during a controlled drying period at 20° C.-100° C. during which said adsorbed ethanol blocking liquid migrates outwardly toward the surface of said porous ceramic carrier layer during drying and minimizes migration of said aluminum tri-isopropoxide sol into said porous ceramic carrier layer as drying continues thereby forming a dried porous ceramic carrier layer bearing a surface layer of dried aluminum tri-isopropoxide sol; calcining said porous ceramic carrier layer bearing said surface layer of dried aluminum tri-isopropoxide sol at a calcining temperature of 400° C.-500° C. thereby decomposing said aluminum tri-isopropoxide and forming a porous carrier layer bearing a surface layer of decomposed aluminum tri-isopropoxide sol; and recovering said porous ceramic carrier layer bearing a surface layer of decomposed aluminum tri-isopropoxide sol.

Claim 17

The method of preparing a membrane assembly containing (i) a porous ceramic carrier layer characterized by mechanical strength and (ii) a porous surface layer which comprises loading the outer layers of macropore of a porous ceramic carrier with ethanol blocking liquid thereby forming a porous ceramic support layer bearing outer layers of macropores loaded with adsorbed blocking liquid; contacting said outer layers of macropores of said porous ceramic carrier layer loaded with said ethanol adsorbed blocking liquid with an aluminum tri-isopropoxide sol; maintaining said outer layers of macropores of said porous carrier layer loaded with said ethanol adsorbed blocking liquid in contact with said aluminum tri-isopropoxide sol for an adsorption period during which said sol is adsorbed as a surface layer on the surface of said porous carrier layer; drying said porous support layer bearing (i) outer layers of macropores loaded with said ethanol adsorbed blocking liquid and (ii) a surface layer of said aluminum tri-isoproxide sol during a controlled drying period at 20° C.-100° C. during which said adsorbed ethanol blocking liquid migrates outwardly toward the surface of said porous ceramic carrier layer during drying and minimizes migration of said aluminum tri-isopropoxide sol into said porous ceramic carrier layer as drying continues thereby forming a dried porous ceramic carrier layer bearing a surface layer of dried aluminum tri-isopropoxide sol; calcining said porous ceramic carrier layer bearing said surface layer of dried aluminum tri-isopropoxide sol at a calcining temperature of 400° C.-500° C. thereby decomposing said aluminum tri-isopropoxide and forming a porous carrier layer bearing a surface layer of decomposed aluminum tri-isopropoxide sol; and recovering said porous ceramic carrier layer bearing a surface layer of decomposed aluminum tri-isopropoxide sol.